GB2028163A - Apparatus for the separation and recovery of a solid producttransported by a gas - Google Patents

Apparatus for the separation and recovery of a solid producttransported by a gas Download PDF

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Publication number
GB2028163A
GB2028163A GB7927291A GB7927291A GB2028163A GB 2028163 A GB2028163 A GB 2028163A GB 7927291 A GB7927291 A GB 7927291A GB 7927291 A GB7927291 A GB 7927291A GB 2028163 A GB2028163 A GB 2028163A
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GB
United Kingdom
Prior art keywords
filter
chamber
gas
cartridge
walls
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
GB7927291A
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GB2028163B (en
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Commissariat a lEnergie Atomique et aux Energies Alternatives CEA
Original Assignee
Commissariat a lEnergie Atomique CEA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Commissariat a lEnergie Atomique CEA filed Critical Commissariat a lEnergie Atomique CEA
Publication of GB2028163A publication Critical patent/GB2028163A/en
Application granted granted Critical
Publication of GB2028163B publication Critical patent/GB2028163B/en
Expired legal-status Critical Current

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Classifications

    • G—PHYSICS
    • G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/02—Treating gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0084—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours provided with safety means
    • B01D46/0091—Including arrangements for environmental or personal protection
    • B01D46/0094—Including arrangements for environmental or personal protection against radiation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2411—Filter cartridges
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/58—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/66—Regeneration of the filtering material or filter elements inside the filter
    • B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2265/00—Casings, housings or mounting for filters specially adapted for separating dispersed particles from gases or vapours
    • B01D2265/06—Details of supporting structures for filtering material, e.g. cores
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S55/00—Gas separation
    • Y10S55/09—Radioactive filters

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Toxicology (AREA)
  • General Engineering & Computer Science (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Geometry (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Air Transport Of Granular Materials (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

1 GB2028163A 1 SPECIFICATION i 50 Apparatus for the separation and
recovery of a solid product transported by a gas The present invention relates to an apparatus for the separation and recovery of a solid product transported by a gas and usable more particularly for the recovery of radioactive par- ticles, such as plutonium oxide powder present in a gas flow.
More specifically it relates to a separation apparatus having at least one filter cartridge made from a porous material into which is introduced the gas transporting the solid product to be separated in such a way as to retain the latter within the cartridge and to purify the gas by passage through the cartridge wall.
The presently known filtering apparatuses of this type generally comprise one or more cylindrical filter cartridges within which circulates the gas transporting the solid product to be separated, the latter then being optionally recovered in a container positioned below the cartridges, which are unclogged for example by means of a gas counterflow or by mechanical shaking or by both these actions together.
Static apparatuses of this type have the disadvantage of not being usable with corn- plete safety and under completely satisfactory reliability conditions for carrying out the separation of fissile products transported by pneumatic means or radioactive products when they are constituted by materials which are degraded under the action of radiation or heat. In the case of fissile products the geometry conditions which have to be fulfilled lead to difficulties in connection with the flow and recovery of the powders, as well as to un- clogging problems.
The present invention relates to an apparatus for the separation and recovery of a solid product transported by a gas and which obviates the above disadvantages.
The present invention therefore relates to an apparatus for the separation and recovery of a solid product transported by a gas, wherein it comprises at least one filter cartridge made from a rigid porous material mounted in a sealed enclosure and defining in the latter a first filter chamber within the cartridge and which communicates by its lower end with a tube for the collection of the separated solid product and a second chamber for the collec- tion of the filtered fluid outside the said cartridge, the latter having two large-surface opposite porous walls maintained with an appropriate spacing by spacers fixed on the said walls and disposed in the filter chamber in such a way as to form deflectors, means for introducing the gas transporting the solid product to be separated into the said filter chamber and means for extracting the filtered gas from the collection chamber.
Advantageously the apparatus also corn- prises means for introducing a gas into the collection chamber with a view to ensuring the unclogging of the filter cartridge.
The apparatus as defined hereinbefore has the advantage of being particularly suitable for the separation of particles of fissile products transported by a gas flow. Thus, due to the presence of the spacers which give the filter cartridge assembly completely satisfactory properties as regards mechanical strength and pressure behaviour, said cartridge can have a large filter surface area, whilst defining a thin filter chamber in order to satisfy safety requirements in connection with criticality.
Moreover, the presence of suitably positioned spacers within the filter chamber contributes to the separating action, due to the impact or friction of solid particles thereon.
In addition, said apparatus also has the advantage of being able to operate in a corrosive atmosphere, at elevated temperature and in the presence of radioactive substances, because the complete apparatus can be made from a corrosion-resistant, radiation- resistant and heat-resistant material, e.g. stainless steel.
According to a preferred embodiment of the apparatus according to the invention the filter cartridge has, at least in its lower part, a cross-section which increases rapidly from its lower end to its upper end.
Preferably, in this embodiment, the two opposite porous walls of the filter cartridge are parallel and, at least in their lower parts, substantially have the shape of a triangle, whose apex is directed towards the lower end of the catridge and whose two walls are joined together at least on their lateral edges by porous material elements.
This embodiment of the apparatus according to the invention is particularly advantageous because, by introducing the gas flow which transports the solid product to be separated into a filter chamber whose cross-section increases rapidly in the vicinity of the gas flow inlet, a rapid decrease in the speed of the gas flow is brought about, which improves the separating action obtained.
Moreover, when in this embodiment the apparatus comprises means for introducing a gas into the collection chamber during the unclogging of the filter cartridge under the action of the gas introduced into said chamber it is possible to recover the separated solid product in the filter chamber by making it drop freely onto a highly sloping fluidised bed which converges towards the collection tube.
In this case, during unclogging, a gas is introduced into the collection chamber under a pressure which is selected as a function of the slope of the filter cartridge walls in order to create on the latter a fluidised bed, in such a way that the powder which has fallen onto the inclined walls of the cartridge drops in the form of a fluidised bed towards the extraction 2 GB2028163A 2 tube and consequently towards a recovery tank. The gas is introduced in such a way that it creates a distributed gas flow perpendicular to the wall.
According to another feature of the apparat us according to the invention the spacers advantageously comprise an undulating plate provided with openings, or an undulating plate in which there are inlets, said undulating plate being alternately connected by the apex of said undulations with both the said walls in such a way as to form in the filter chamber vertically extending channels, whilst ensuring a good mechanical performance of the apparatus.
According to a variant the spacers comprise profiled members mounted between the walls in such a way as to oppose the rising of the solid product into the filter chamber and so as to ensure a good mechanical performance of the assembly.
Advantageously these members are shaped like triangular prisms and are arranged in rows between the walls, the members of one row being staggered relative to the members of the adjacent row and each member in one row is oriented in such a way that one of the lateral faces of the prism is surmounted by a ridge.
The invention is described in greater detail 95 hereinafter with reference to non-limitative embodiments and the attached drawings, wherein show:
Figure 1 a diagrammatic perspective repre- sentative of the apparatus according to the invention.
Figure 2 a first embodiment of the spacers mounted in the filter cartridge of the apparat us according to the invention.
Figure 3 a second embodiment of the spa- 105 cers.
Figure 4 a third embodiment of the spacers.
Figure 5an apparatus according to the invention in which several filter cartridges are arranged in parallel.
Figure 6 an apparatus according to the invention in which a number of filter cartridges are mounted in series.
On referring to Fig. 1 it is possible to see that the apparatus according to the invention comprises an enclosure 1 within which is vertically mounted a filter cartridge 3. The enclosure 1 is made, for example, from mechanically welded sheets provided with exter- nal reinforcements and of appropriate thickness to resist pressure and vacuum forces, whilst it is closed in its upper area by a sealed or detachable cover 5 provided with an outlet 7, sealing between enclosure 1 and cover 5 being ensured by a joint 9.
The rigid filter cartridge 3 is sealingly mounted by means of a joint 16 and defines in enclosure 1 a first filter chamber 11 within the cartridge and a second collection chamber 13 outside the cartridge and surrounding the latter.
The filter chamber 11 communicates by its lower end which is in the form of a pipe 3c, with a collection tube 17 into which issues a duct 19 for the introduction of the gas transporting the solid product to be separated.
Advantageously duct 19, collection tube 17 and pipe 3c are arranged so as to form a cyclone, which also participates in the separa- tion of the solid particles.
Two ducts 21 open out onto the side walls of the enclosure and by means of said ducts it is possible to introduce into collection chamber 13 a gas flow in order to bring about the unclogging of the filter cartridge 3.
According to the invention filter cartridge 3 has two large surface area opposite walls 31 and 32 maintained with a desired spacing by spacers 23 welded to the said plates and provided within the filter chamber 11 on the one hand for improving the mechanical behaviour of the filter cartridge, particularly the strength of walls 31 and 32 with a view to withstanding overpressures and vacuum and on the other hand to act as deflectors in the path of the gas flow circulating in said chamber.
In the embodiment illustrated in this drawing walls 31 and 32 are also maintained parallel to one another and in their lower portion are essentially shaped like a large area triangle, whose apex is connected to pipe 3c. Thus, filter chamber 11 has a small crosssection in the vicinity of the gas inlet trans- porting the solid product to be separated and its cross-section regularly and rapidly increases up to the vicinity of its upper end 3b. Moreover, it should be noted that these walls constitute large filtering surfaces which can be maintained at a limited spacing in order to satisfy requirements when the apparatus is to be used for separating radioactive or fissile products.
A rigid filter cartridge of this type can for example be made from two plates of porous material substantially shaped like a triangle in their lower part and shaped like a rectangle in their upper part, said plates being interconnected on their lateral edges and at their upper end by members made from the same porous material in order to form a filter cartridge closed at its upper end and open at its lower end.
Optionally the filter cartridge can be directly closed at its upper end by cover 3 and in this case outlet 7 is positioned on one of the side walls of the enclosure.
The porous material used for the manufacture of the filter cartridge is chosen as a function of the nature of the gas and the solid product to be separated and it has porosity and permeability characteristics adapted to the size of the particles of the solid product to be recovered. This rigid material can be in the form of a porous or alveolar metal, for exam- 4 3 GB2028163A 3 pie fritted stainless steel.
The apparatus functions in the following manner. The gas transporting the solid prod uct to be separated is introduced by duct 19.
This gas then rises in the filter chamber 11 in which the particles are separated on the one hand level with the filter cartridge walls and on the other in the filter chamber under the action of the rapid reduction in the speed of the gas flow and the effects of impacts and friction of the particles on spacers 23. The filtered gas is collected by following the direc tion of arrows F, in collection chamber 13 and is then evacuated by outlet 7, whilst the solid particles are recovered in collection tube 17.
In order to ensure the unclogging of the cartridge the introduction of the gas flow transporting the solid product to be separated the introduction of the gas transporting the is interrupted and outlet 7 is blocked, after 85 solid product to be separated.
which a gas counterflow is introduced through It should be noted that enclosure 1 has a ducts 21 and by following arrows F2 ensures single outlet 7 and two or more ducts 21 the unclogging of the filter cartridge and the (only one of which is visible in the drawing) discharge of the solid product into tube 17. for introducing a gas counterflow in order to The powder expelled by the gas counterflow 90 bring about the unclogging of all the filter and suspended in the filter drops towards the cartridges.
bottom of the latter. Thus, it is directed to- Fig. 6 shows an apparatus according to the wards the inclined rigid porous material pas- invention in which a plurality of filter car sages which converge towards the powder tridges 3 are mounted in series in an enclo- extraction pipe 3c. The pressure necessary for 95 sure 1. In this case enclosure 1 is provided the unclogging of the filter produces in said with separating members 29 which define a passage, as over the complete surface of the chamber for the collection of the filtered gas porous material, a distributed gas flow per- around each filter cartridge 3 and these collec pendicular to the wall preventing the powder tion chambers are in each case provided with from being redeposited in the form of a pile or 100 a corresponding outlet 7 and ducts 21 for the from being reabsorbed by the filtering subintroduction of an unclogging gas coun strate of the said passage. The flow rate and terflow.
direction of this gas flow are such that in this way a fluidised bed is formed which makes the powder drop towards the extraction pipe 3c and therefore towards the recovery tank. After unclogging the gas is discharged through outlet 7.
On referring to Fig. 2 it can be seen that the spacers are constituted by an undulating plate 23 having circular openings 25, whereby said undulating plate is alternately in contact by the apex of its undulations with the two opposite walls 31 and 32 of the filter catridge and is fixed to the latter, e.g. by spot welding.
Thus, in the filter chamber channels are defined which extend in a vertical direction. The gas transporting the solid product to be separated introduced into filter chamber 11 is firstly directed in the central channels and is then laterally distributed by passage through openings 25. This leads to a certain impact and friction action du'ring the changes of direction and thus aids the separation of the solid product transported by the gas.
Fig. 3 shows a spacer of the same type as in Fig. 2, said spacer also being formed by an undulating plate 23 in which there are inlets 26, which increases the impact action of the solid particles on the spacers.
Fig. 4 shows another embodiment of the spacers, which comprise profiled members 28 shaped like triangular prisms mounted be- tween the two opposite walls 31 and 32 in such a way as to form rows in which the members of one row are staggered with respect to the members of adjacent rows. The members 28 are oriented in such a way that one of the faces of prisms 28 is surmounted by a ridge 28b. This orientation has the advantage of aiding, during unclogging, the dropping of the solid product towards the collection tube.
Fig. 5 shows an apparatus having a plurality of filter cartridges 3 mounted in parallel in the same enclosure 1, each being associated with a collection tube 17 and a duct 19 for It should be noted that the outlet 7 of a collection chamber associated with a filter cartridge is connected to the inlet 9 of the following filter cartridge so as to successively pass the gas transporting the solid product to be separated into all the filter cartridges of the apparatus, thus improving the separating efficiency.

Claims (12)

1. An apparatus for the separation and recovery of a solid product transported by a gas, wherein it comprises at least one filter cartridge made from a rigid porous material mounted in a sealed enclosure and defining in the latter a first filter chamber within the cartridge and which communicates by its lower end with a tube for the collection of the separated solid product and a second chamber for the collection of the filtered fluid outside the said cartridge, the latter having two large-surface opposite porous walls main- tained with an appropriate spacing by spacers fixed on the said walls and disposed in the filter chamber in such a way as to form deflectors, means for introducing the gas transporting the solid product to be separated into the said filter chamber and means for 4 GB2028163A 4 extracting the filtered gas from the collection chamber.
2. An apparatus according to claim 1, wherein it comprises means for introducing a gas into the collection chamber in order to ensure the unclogging of the filter cartridge.
3. An apparatus according to claim 1, wherein the filter cartridge is shaped in such a way that it defines a fitter chamber having, at least in its lower part a cross-section which increases rapidly from its lower end to its upper end.
4. An apparatus according to claim 2, wherein the filter cartridge has a shape such that it defines a filter chamber having, at least in its lower part a cross-section which increases rapidly from its lower end to its upper end in such a way that during the unclogging of said filter cartridge by introducing a gas into the collection chamber it is possible to recover the said solid product by displacing it on a fluidised bed converging towards the collection tube.
5. An apparatus according to either of the claims 3 and 4, wherein the opposite porous walls of the filter cartridge are parallel and, at least in their lower part, are substantially shaped like a triangle whose apex is directed towards the lower end of the cartridge, said walls being interconnected at least on their lateral edges by porous material members.
6. An apparatus according to any one of the claims 1 to 5, wherein the spacers are constituted by an undulating plate provided with openings and which is alternately connected by the apex of said undulations with both the said walls in such a way as to form in the filter chamber channels which extend in a vertical direction and ensure a good me- chanical behaviour of the complete apparatus.
7. An apparatus according to any oneof the claims 1 to 5, wherein the spacers cornprise an undulating plate in which there are inlets, each undulating plate being alternately connected by the apex of the said undulations with both the walls in such a way as to form in the filter chamber vertically extending channels ensuring a good mechanical behaviour of the complete apparatus.
8. An apparatus according to any one of the claims 1 to 5, wherein the spacers cornprise profiled members mounted between the walls in such a way as to oppose the rising of the solid product in the filter chamber, whilst ensuring a good mechanical behaviour of the complete apparatus.
9. An apparatus according to claim 8, wherein the said members are shaped like a triangular prism and are arranged in rows between the wails, the members of one row being staggered relative to the members of the adjacent row and each member in one row being oriented in such a way that one of the faces of the prism is surmounted by a ridge, said spacers also ensuring the satisfac- tory mechanical behaviour of the complete apparatus.
10. An apparatus according to any one of the claims 1 to 9, wherein it comprises a plurality of filter cartridges mounted in parallel in the enclosure.
11. An apparaus according to any one of the claims 1 to 9, wherein it comprises a plurality of filter cartridges mounted in series in the enclosure, at least one separating member positioned within the enclosure so as to define a chamber for the collection of the filtered gas associated with each filter cartridge and means for introducing into the filter chamber defined by a filter cartridge the gas extracted from the collection chamber associated with the preceding cartridge.
12. An apparatus substantially as described hereinbefore with reference to the drawings.
Printed for Her Majesty's Stationery Office by Burgess & Son (Abingdon) Ltd-1 980. Published at The Patent Office, 25 Southampton Buildings, London, WC2A 1AY, from which copies may be obtained.
GB7927291A 1978-08-11 1979-08-06 Apparatus for the separation and recovery of a solid producttransported by a gas Expired GB2028163B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7823737A FR2432883A1 (en) 1978-08-11 1978-08-11 DEVICE FOR SEPARATION AND RECOVERY OF A SOLID PRODUCT CARRIED BY A GAS

Publications (2)

Publication Number Publication Date
GB2028163A true GB2028163A (en) 1980-03-05
GB2028163B GB2028163B (en) 1982-09-02

Family

ID=9211794

Family Applications (1)

Application Number Title Priority Date Filing Date
GB7927291A Expired GB2028163B (en) 1978-08-11 1979-08-06 Apparatus for the separation and recovery of a solid producttransported by a gas

Country Status (6)

Country Link
US (1) US4261713A (en)
JP (1) JPS5526197A (en)
BE (1) BE878196A (en)
DE (1) DE2932365A1 (en)
FR (1) FR2432883A1 (en)
GB (1) GB2028163B (en)

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GB2229938A (en) * 1989-04-04 1990-10-10 Pall Corp Gas filter
US5358552A (en) * 1992-07-30 1994-10-25 Pall Corporation In situ filter cleaning system for gas streams

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US4730647A (en) * 1986-12-08 1988-03-15 Nordson Corporation Powder feeder apparatus
ES2101749T3 (en) * 1990-08-03 1997-07-16 Sanko Ind Corp PROCEDURE, DEVICE AND SYSTEM FOR THE TREATMENT OF EXHAUST GASES.
US5287591A (en) * 1992-03-30 1994-02-22 Racine Industries, Inc. Carpet cleaning machine with convertible-use feature
DE69224666T2 (en) * 1992-03-30 1998-06-25 Racine Ind Inc CARPET CLEANING MACHINE FOR PARTICLE REMOVAL
US5928396A (en) * 1997-12-31 1999-07-27 Aaf International Pocket filter and method and apparatus for making the same
DE29800969U1 (en) 1998-01-22 1998-04-16 Kluge Klaus Dipl Ing Spacer system for pocket filters
SE527578C2 (en) * 2004-05-26 2006-04-11 Absolent Ab Filter cartridge consisting of a housing surrounding a pleated filter mat with spacers between parallel opposite filter mat parts
JP4785570B2 (en) * 2006-03-13 2011-10-05 日本バイリーン株式会社 Windsock filter and manufacturing method thereof
DE102006061256B4 (en) * 2006-12-22 2009-04-30 Fette Gmbh Filter system for separating dusts from gases
DE102010045000A1 (en) * 2010-09-10 2012-03-15 Herding Gmbh Filtertechnik Filter device and filtering method
US10176901B2 (en) 2013-08-14 2019-01-08 Ge-Hitachi Nuclear Energy Americas Llc Systems, methods, and filters for radioactive material capture
US9812229B2 (en) 2014-03-04 2017-11-07 Paschal-Gross Enterprises, Inc. Safe geometry vacuum design

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Publication number Priority date Publication date Assignee Title
GB2229938A (en) * 1989-04-04 1990-10-10 Pall Corp Gas filter
GB2229938B (en) * 1989-04-04 1993-09-15 Pall Corp Filtration system and method
US5318606A (en) * 1989-04-04 1994-06-07 Pall Corporation Filtration system
US5358552A (en) * 1992-07-30 1994-10-25 Pall Corporation In situ filter cleaning system for gas streams

Also Published As

Publication number Publication date
GB2028163B (en) 1982-09-02
FR2432883B1 (en) 1982-10-22
BE878196A (en) 1979-12-03
FR2432883A1 (en) 1980-03-07
JPS5526197A (en) 1980-02-25
DE2932365A1 (en) 1980-02-21
JPS6344409B2 (en) 1988-09-05
US4261713A (en) 1981-04-14

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